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- 6.1 Determine the heat transfer coefficient at the stagnation point and the average value of the heat transfer coefficient for a single 5-cm-OD, 60-cm-long tube in cross-flow. The temperature of the tube surface is , the velocity of the fluid flowing perpendicular to the tube axis is 6 m/s, and the temperature of the fluid is . Consider the following fluids: (a) air, (b) hydrogen, and (c) water.6.3 Steam at 100 kPa and is flowing across a 5-cm- OD tube at a velocity of 6 m/s. Estimate the Nusselt number, the heat transfer coefficient, and the rate of heat transfer per meter length of pipe if the pipe is at .determine the length of the tube required for fully develop flow when 9.06 kg of waterper minute is passed through a tube of 2 cm, it is found to be heated from 20 degree celsiusto 60 degree celsius, the heating is achieved by considering steam on the surface of the tube andsubsequently the surface temperature of the tube is maintained at 90 degree celsius.
- 3. Two parallel plates are separated by a distance 2H. The plates are moved in opposite directions with constant velocity Uo. Each plate is maintained at uniform temperature To. Taking into consideration dissipation, determine the heat flux at the plates. Assume laminar flow and neglect gravity effect. To U. Uo T.2. A rod of radius ni is placed concentrically inside a sleeve of radius ro. Incompressible fluid fills the clearance between the rod and the sleeve. The sleeve is maintained at uniform temperature To while rotating with constant angular velocity o. Taking into consideration dissipation, determine the maximum fluid temperature and surface heat flux at the sleeve. Assume incompressible laminar flow and neglect end effects. stationaryair at constant pressure of 101.3kpa and 289 k enters inside a tube having an inside diameter of 19.1 mm and a lenght of 2.12m with a velocuity of 24.4m/s. condensing steam on the outside of the tube maintanis the insde wall temprature at 373.1 k knowing that the air flow is turbulent calculate the convection coefficient of the air . ( hint use the simplifiled equaation for air at 1 atm)
- You are designing a pin-style heatsink for forced cooling of an IC. A small fan blows RT air into the heatsink at about 2.3 ? ? . The aluminum pins are 2mm in diameter and have a constant surface temperature of 120°?. The heatsink is 100mm x 100mm and the pins have an inline arrangement with a transverse pitch of 4mm and a longitudinal pitch of 6mm. What is the total heat dissipation of this heatsink? The pins are 30mm high. Note RT=25 celsiusCorsidera circular smoth pipeof inner diameter D;=0.015mwhose inner surface is covered with a layer of liquid as a result of condensation. In order to dry the inner surface of the pipe, air at 300K at 1 atmis forced to flow throughit with anaverage velocity of 1.2m/s. Using the analogy between heat and mass trarsfer, detemine the mass transfer coeffícient irside the pipe for fully developed flow. Note: Viscosity of the air for given conditions is given as 1.58 x 10°n?/s. Also, for a lamirar fully developed flow the N=Sh=3.66. Your solution must state governing equations and associated assumptions, illustration and step by step execution of the overall solutionConsider pressurized water, engine oil (unused), and Nak (22%/78%) flowing in a 20-mm-diameter tube. (a) Determine the mean velocity, in m/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for each of the fluids when the fluid temperature is 366 K and the flow rate is 0.01 kg/s. (b) Determine the mass flow rate, in kg/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for water and engine oil at 300 and 400 K and a mean velocity of 0.022 m/s. Part A Determine the mean velocity, in m/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for each of the fluids when the fluid temperature is 366K and the flow rate is 0.01 kg/s. Liquid Um (m/s) Xfdh (m) Xfd,t (m) water i engine oil i i i Nak i
- Only answer if you are 100% sure otherwise i will downvote... An ASTM B75 copper tube sheathes a heating element that is used to boil water at 1254 kPa. The copper tube is immersed horizontally in the water, and its surface is polished. The tube diameter and length are 5 mm and 9.5 cm, respectively. The maximum use temperature for ASTM B75 copper tube is 204°C. Determine the highest evaporation rate of water that can be achieved by the heater without heating the tube surface above the maximum use temperature. Use the property tables to calculate the properties of water at saturation temperature. The surface tension 0 at 190°C is 0.03995 N/m. Also, Csf 0.0130 and 10 for the boiling water on a polished copper surface. The highest evaporation rate of water is g/s?When oil and gas flow in vertical pipes, and the flow regimes is bubble flow then the continuous phase is Oil Gas 50% Oil and 50% Gas O No continuous phase existsWater is to be boiled at atmospheric pressure in a polished copper pan by means of an electric heater. The diameter of the pan is 0.48 m and is kept at 108 deg C. What is the power required to boil the water? Tsat 100°C; Properties of water at 100°C: Density. pl= 961 kg/m3; Kinematic viscosity, v 0.293x10-6 m2/s: Prandti Number. Pr 1.740; Specific heat, Cpl = 4216 J/kg.K; Dynamic viscosity, u = p x v = 961 x 0.293 x 10-6 = 281.57 x10-6 Ns/m2; hfg = 2256.9 k/kg; pv = 0.597 kg/m3; a = 0.0588 N/m; Csf=0.013; n=1: